How It Works

Darcy-Weisbach Equation

The Darcy-Weisbach equation is the fundamental formula for calculating pressure drop due to friction in pipe flow:

dP = f * (L/D) * (rho * V^2 / 2)

Where: dP = pressure drop, f = Darcy friction factor, L = pipe length, D = inside diameter, rho = fluid density, V = flow velocity

Reynolds Number

The Reynolds number determines the flow regime and is essential for calculating the friction factor:

Re = (V * D) / v

Where: V = velocity, D = diameter, v = kinematic viscosity (cSt * 10^-6)

  • Laminar (Re < 2,300): Smooth, parallel flow layers. f = 64/Re
  • Transitional (2,300 < Re < 4,000): Unstable, unpredictable flow
  • Turbulent (Re > 4,000): Chaotic flow with eddies. Use Colebrook equation

Friction Factor (Moody)

For laminar flow: f = 64 / Re

For turbulent flow, the Colebrook-White equation is used (solved iteratively):

1/sqrt(f) = -2*log10(e/3.7D + 2.51/(Re*sqrt(f)))

For smooth hydraulic hose, the relative roughness (e/D) is typically 0.000005 to 0.00001.

Pressure Drop in Hydraulic Lines Q P1 P2 Pressure Drop (dP = P1 - P2) Length (L) ID dP = f * (L/D) * (rho * V^2 / 2)

Key Factors Affecting Pressure Drop

  • Velocity: Pressure drop increases with velocity SQUARED
  • Viscosity: Higher viscosity = higher friction (especially in laminar flow)
  • Length: Pressure drop is directly proportional to length
  • Diameter: Pressure drop is inversely proportional to D^5

Pressure Loss Calculator

Calculate pressure drop in hydraulic lines using Darcy-Weisbach equation with Moody friction factor.

Smooth hose: 0.000005", Steel tube: 0.00006"

Fluid Properties

At operating temperature
Typical hydraulic oil: 7.2 lb/gal
Turbulent Flow
Re = --

Pressure Loss Results

Pressure Drop --
Pressure Drop (alternate) --
Reynolds Number --
Flow Regime --
Darcy Friction Factor --
Flow Velocity --
Relative Roughness (e/D) --
Drop per 10 ft --
Drop per 100 ft --

Hydraulic Fluid Properties

Fluid Viscosity @ 40C Viscosity @ 100C Density
ISO VG 32 32 cSt 5.4 cSt 0.87 kg/L
ISO VG 46 46 cSt 6.8 cSt 0.87 kg/L
ISO VG 68 68 cSt 8.7 cSt 0.88 kg/L
ATF (Dexron) 35 cSt 7.5 cSt 0.85 kg/L
Water 0.66 cSt 0.29 cSt 1.0 kg/L

Note: Viscosity varies significantly with temperature. Use actual operating temperature viscosity for accurate results.

Design Guidelines

Maximum recommended pressure drop: 5% of system pressure
Suction line max drop: 3-5 psi (0.2-0.35 bar)
Return line typical drop: 10-30 psi (0.7-2 bar)